Publication Date:
2011-12-31
Description:
Simulation of a single tube of a wall-cooled multitubular Fischer-Tropsch (FT) reactor with a cobalt catalyst indicates that the reactor performance is improved by enlarging the catalyst particle diameter. This aspect is studied for variation of the particle size for a fixed tube diameter and vice versa. For a syngas conversion per pass of about 30 % as target and a typical industrially used single-tube diameter of 40 mm, a particle size of 〉 3 mm is appropriate with regard to a high production rate of higher hydrocarbons. For a particle diameter of 〈 3 mm, a temperature runaway can only be avoided by rather low cooling temperatures, and the target conversion cannot be reached. In addition, the pressure drop then gets rather high. The reasons for this behavior are: (i) the heat transfer to the cooled tube wall for a given tube size is considerably enhanced by increasing the particle size; (ii) the influence of pore diffusion on the effective rate gets stronger with rising particle size which decreases the danger of temperature runaway. Detailed simulation of the influence of the catalyst particle size on the behavior of a multitubular Fischer-Tropsch reactor with regard to syngas conversion and production rate of hydrocarbons per tube in a wall-cooled single tube with cobalt as catalyst indicates that the reactor performance is improved by enlarging the catalyst particle diameter. Reasons for this unexpected behavior are evaluated.
Print ISSN:
0930-7516
Electronic ISSN:
1521-4125
Topics:
Chemistry and Pharmacology
,
Process Engineering, Biotechnology, Nutrition Technology
